Oil distillation and cracking



lfxatented Il 19427.l

A-T'ES' 4srrnrnrav L. TINGL'EY, ormrno, weer' v incmmnl on. nrs'rifLATroN 'AND Cienciano;

Ainnemen mail,V December 28, I132?.- i'sefil lie- 68'3163- This invention relates to' improvements in '51 'oil crackin and distillation apparatus and the genera object thereof isle-provide a more effective apparatus for they cracking .and distillation of hydrocarbon zoils, which will enable the complex hydrocarbon mole-- c'ules to be broken up at lower temperatures than are usually 'required in oilV cracking 4 and distillation apparatus-aud also whichments upon theapparatus disclosed in my -will maintain-a. more even and perfect pro-A.

:duction of a desiredfdistillationproduct. if The inventioncomprises certain -improvejprior 'application Serial Nu1nber668,229 filed *October- 3,125- 1923, iu'ivhich a jacketed coil is locatedin and extends preferably longitu which-surrounds the oil' conduit issu er-.

he.l` .superheated steam' which, surrounds the oil -dinally'of'the furnace, oil being supplied lto -"the central coil o'r conduit and steam to the jacket ofthe' coil. In this construction the' eiland steam arevap'orized Aduring their pas- Asage through the furnace and thesteam heated to a lvery `high"temperaturc.

conduit'heats thejoil vapor in 'the conduit to substantiall which issu cient to crack the more complex molecules of the hydrocarbon. The eiland ja regulated portion of the steanr are ther dischar ed into a-mixing chamber tromV whicht ley arecarried intol a fixationchamber and retained in said 4fixation' cham-v 4b er a suiiieient time to permanently iix the pro'duetffwhiehis then carried to a suitable condensing and storage apparatus.

One of the objects 'of the present invention V is to p ovide means 'forsubje'cting the voil and wa er, before the same enter the coil and acke t, respectively to the inliuence 'of vfiferation of'distillation and crackina.

ioactive material to' facilitate the op- A flirtherobject of the invention is to providerneans for subjecting the highlyheated o l vapor to radioactivity either by subjectgactive substance or to the action of the ultraing the oil vapor to emanations from aradio- -voilet 'ravs or both-prior to the ,introduction :of .th'eoil vapor into the mixing chamber. -fui'ther object of' the invention is to rovide means for subjecting the super -lieatedsteam to the action of a catalyst, or a Y "I substance 'acting in the natlll- Ufl aux,

prior' to itsintroduetion. into the' mixing I' chamber'in order to assist inbreakng 'up- A the-molecules of the dsuperheate'd steam into the same high, temperature ings and will their constituent el'ementsl hydrogen i and, oxygen. I

. A. further object of the invention to"proheated-steamand highly heated' h drocar onvapor, in which more 4or less of tie com lex molecules' of the hydrocarbon have lvide means by' which a' mixture of su ercracked; maybe subjected, while in such i mixed state, to radioactivity either by emanations from a radioactive substance or to the action of. the ultra-violet ray, or both, prior. to the entry into the mixing chamber.

A further object of the invention is'to provide. means for subjecting the mixed steam and hydrocarbon vapors to the actiony of alea talys'tz preferably prior to the entry intoV the mixing chamber rfurther to facili chemical reaction between the elements of itate the necessary chemical reactions re quired to crack themore resistant complex vhydrocarbon molecules 'and to cause such the dissociated molecules as' will produce a :l

.desired product.

-.A further object of thel invention is to Vprovide a steam jacket surrounding the mixing :chamber and also a steamjjacket'surrounding the fixation chamber vwhich will 4protect the walls of the mixingand fixation chambers. -respectively -ir'oxn direct con let with the llames or heatnof the furnace thereby preventing,carbonization uppn the inner walls of themixing and fixation chambers.l @A further object of. the invention is 44to provide means-for controlling the fluctuations of the liquid: level of the oil andy preferably alsoof the water in the conduits which fluctuatio'nis' likely to be caused b generation Y of va or below the surface of t e oil \\hicl 1` will orcether-column 'of liquid u wardly.

' 'Other objects-and features o the inven- -tion will more fully appear. from the following description vand the accompanying draw' .y

containing the jacketed coils for the-hydrocarbon and-its vapors, the water and its superheated steam,4 and illustrating alsothe means for subjecting they oil and Waterre spectively to emanations preferably'a beta ray from a radioactive substance `such as 11o uranium oxide, and also illustrating the preferred foi-ins of apparatus for subjectingthe highly heated hydrocarbon vapors and the super ieated steam to radioactivity either in the forni of ci'nanations ,preferably a beta,

. or in mixed condition in one or more of'suc i apparatus.

The apparatus illustrated in the-drawings may be'and preferably is similar to that disclosed in my prior ap lication aforesaid and comprises a n'eferab y c llndrical v ertical furnace 1, of rick with a iningof fire brick or other siii-table refractory material, provided with a fire-box extension 2, preferably of the Dutch oven type into which a gas or oil burner 3 extends. A pipe 4 for the oil leads into the furnace and is surrounded by an outer concentric pipe 5 which forms a jacket for the oil pipe. The inner and outer' pipes are formed into a cylindrical` coil 6 which may be rf any desired diameter and "contain any desired number of turns.

As illustrated herein the coil 6 is formed in a seriesl of superposed sections 7 which, for convenience in construction, are sepa lately supported upon a series of projections or ledges projecting inwardly from the wall of the furnace. The sections of the jacket r pipe are joined by suitable connections 8 Awhich ma 'extend outside of the furnace wall as il ustrated or may be housed in a recessin the wall asdesired. The sections of the oil pipe likewise are joined by connections 9 in a similar manner .tothe connec-' tions of the sections of the jacket.

Any suitable means may be provided for.

supplying oil to the inner pipe or coil and water to the outer pipe or jacket. As illustrated herein tanks 10 and 11 are mounted above or upon the fire-box, the tank 1 0 being connected with the oil pipe 4 by a, pi e 12 provided with a suitable regulating va ve 13 to control the quantity of oil supplied. A suitable branch pi e is'provided to permit the oil to be passe through an apparatus in which the oil is subjected to radioactivity as will hereinafter be more fully described'.

The tank 11 is connected to the outer or jacket coil 5 biy a pipe 14 equipped with a regulating va ve 15 by which the quantity of water admitted may be regulated and through which the water ina be passed diiectly to said jacket. A suita le branch pipe is also provided through which the water may be carried toa suitable apparatus for subjecting the same to radioactivity before its introduction into the jacket 5 as will hereinafter more fully appear. 4

.connected at the t'op of the upper sei'tion of the -coil respectively to bianches 16 and 1,7 which, by means of suit-able connections, are united to a pipe 18 which extends downwardly through thetop of the furnace intoa mixing chamber and terminates Inear the bottom of the mixing chamber, suitable reg ulating valves being provided so that a predetermined amount of oil vapor and superheated steam may be introduced into the mixing chamber." A b '-pass 19 connects the branch 17, .though which the superheatcd steam is delivered, to the branch 16 of the oil pipe and is provided with a valve 20 by means of which super-heated steam may be passed through the inner or oil pipe in a downward direction for the cleaning the oil pipe.

The mixture ofhighly heated hydrocarbon' vapor and. superheated steam 'passes from the' pipe 18 heretofore described into theliott-'oni portion of a mixing chamber 21 which is preferably located inthe upper part of the furnace and eoncentrically with the uppermost coil. A drain pipe 22, commu nicating with the bottom portion of the purpose of niixingchan'ib'er and having a suitable valve' 23, provides means by which anyresidue,

which collectsv in be removed.

l'lhe mixing 'chamber desirably has a series of annular bullies 24 which project inwardly from the wall thereof and overlap intermediate annular bullies 25 which are supported upon an outlet pipe 26 which eX- tends from the upper portion of the mixing chamber downwardly through the bottom thereof and delivers the gases from the miic`- ing chamber to the fixation chamber; 4The outer and inner sets of baiiles are in staggered'relation and serve to-force the gaseous products, which are delivered to the mixing chamber, to travel in a eircui tous route from the bottom to bei', thereby thereof.

the mixing chamber, may

insuring" thorough ,mixing The gaseous products which pass' from the mixing chamber through the pipe 26 are .delivered to the lower portion of a prcferthe top of the mixing chamnace and coil and which is so designed as to cause the gaseous products to circulate alternately upwardly and downu-'ardly in thin, sheets until the finally pass upwardly in athin sheet in intimate contact with the outer wall of the fixation chamber which is highly heated. '.lhis is accomplished by providing a series of eoncentrically ar- 'ranged vpartitions having heads providing closures respectively at the lower and upper ends oflthe fixation chamber. As illustrated herein the pipe 26, through which the mixing chamber to the iixation chamber` gaseous'products are delivered from the The oil pipe 4 and the jacket pipe 5 are extendsdownwardly through the top of the I mixing chamber Inearly to the fbottoingof thexation chamber. and the vapors, which are' delivered bythispi e, are `ca\ised to ascend throughjan annu ar space between the pipe26 and n. concentric inner :partition 2 which extends upwardly A1`t1earlv :o the .top vof the chamber; thef-vapors then pass downwardly through the annular space be` tween the inner partitionf27= and a concentric outer partitionfl n'earlxlfffto4 the bottom of :the fixation chamber, thence4 upwardly .through th'c annular space'between the out-'- Y er partition 28fand the outer wall 29 of the.

fixation cliardber,nally leaving thejtop o'fthe .fixatioichalnber 'through a pipe 3U. which extends".tln'ough'thel furnace' 1\ v all v und communicates with n.oonduitlwhieh delivers the fixed` gaseous products to suitablc.

condensing apparatus as' willgbe hereinafter more fully described.

The 'rate of discharge of the `gaseous product .from the fixation chamber is reguated by a; valve 31 iii-the conduit lending to the condensing.apparatus 'and the reslA surein the llixation chamber indicated y a lgauge4 '32. Desirably a pop .sa.fety va'lve 33, or other suitable safety`devi'ce, may be attached to the pipe 30, adjacent to the 30 gauge 32. A pyrometenjt, extending into the pipe 30 in close proximity to the furnacer wall, serves to indicate the temperaq turc of the gaseous roduct leading to thefixation chamber. hns" the operator, by

lation of the amount 'of material suppliedjto the coils and the delivery of the gaseous product from the chamber,"is enabled-'toj- 'lnaintain the proJer condition within the ucta',

n\ean s-=.for controlling the fluctuations o f observation of the'pressure and tem -rature of the fixation chamber 'and slntab e 'reguapparatus-to pro uce the desired prod The apparatus above 'described ma Y und desirably. is like that disclosedi'n-f piorapplication aforesaid. Onezo the objects of the inventiorihasbefore.' stated, is to provide equahzin the liquid'level respectivelyf in the oil pi and in. its jacket. Thisiisacconiplished .of the oil.

connecting a header pi e {i5-fte" certain or a. l? of the connections which u nitethe sections of the oil pipe and providing check v 1 1lv es 4 36 intermediate of the .header and' such con" nections. The function'osaid henderandV check valve. arrangement is to, prevent the sudden raising et the 'liquid'level in theoil pipe due to the foamingof the oil orftoftlie formation of a cushion ofifsteamifrrn the water content of {alle oil'heloji' the.' 's

Bv employing a. headerl 'in 'the manner described the oil which is.:forced upwardly,

by 'either of these causes will. enter-the header by passing the check valves and be. returned to the bottomv of the coil. Like-- wise aheader 137 coinmunicateswith certain' or all of 'the vconnections which unlte the sections of the jackets' for the coil and' are provided. wth checkvalves= 38, this con-- .'structionlikewise -functioning to vprevent the suddeiifrsing of the water level in the jacket by reason of the formation of u cush" 4ion 4ofjstegiin below the surface' of the water whichivould tendzto' force-the 'water upl-wardly 'inl which case thelwater thus orced 1y ein enter the header 37 by pess -ing thecheck valves 38 and be returned to 11p-war the bottom ofthc-jacket. l

' hese headers may be connected to asV many of. the' gonnections for the sections of.- the oil andgwater pi' eas may be desired to control the fluctuation ofy the 'liquid level :of the oil and-water respectively in the coiland jacket.

:Another object cfu-'the invention -is to pro'- -vide means by which :the oil or thewatc'r or both maybe subjected' to .radioactivity bc fore entering the coil 'and jacket. The pur pose-of thussubjectingtheoil tjo .radioac- 4 tivity is to place the 'hydrocarbon molecules into an activated* ctm'diticgll,v thusmaking simple molecules more; easily 'accomplished dissociation thereof-intolghter and more and wit-,hiess expenditure of heat and enf e1'gy. The purpose of .subjccting'th'e water to vradioactivity ,is to' p'lace the water in van :activated condition .by m'cans of which the Vconversitm ofwater intosteam and itssubsequent dissociation into'its constituent eleieu' I .colnplishedincre-readily and 'with n. lessl 'expenditure 'of heat.

4I n the particularappratiisdisclosed here'' in a brunch pipe'.39 extends. downwardly' 10a,- eat'esf with; .an activating apparatus which f 4 Pefln-bly comprisesa cham froinftheoil supply -pipe .12 and communi- 'lindrieal'shell lmerid-provided with headers the oil supply pipe12a the activating 'apparatus describedl--Deslrablythe chamber enclosed vWithin the wall 40 of -the activating apparatus is supplied with steam through a 'suitable inlet pipe 4G and delivered therefrom through an outlet pipe 47. This steam may be supplied in any Suitable valves are provlded inthe oil 12 and its branch 39 to enable the oil either' to be passed directly into the coil or through its lia

. having a series of tubes '50 connecting the header 49 with a header 51, the tubes 50 likewise enclosing tubes 52 containing a radioactive material or bars of radioactive .ma-

.`t eria1, the water being delivered from the .upper header 51 through a pipe 53 to the .supply pipe 14 for the jacket. The chamber 54 which encloses this activating apparatus may, like the chamber which encloses the activating apparatus for the oil, be supplied .with steam for heating the water before it enters the water jacket 5 of the coil.

By reason of the activation of the oil and and itsjacket the oil and water are prepared to be more readily vaporized and dissociated by the lieatof the furnace to which they are subjected during the passage through the furnace and the. temperatures required forvaporization and molecular terially decreased.

A further important object of the invention is to provide means for subjecting the hydrocarbon vapors and the superheated dissociation ma- .steam respectively and selectively, either suwly or in mixed condition, to radioactivity an to other means which will further aid 1n molecular 'dissociation Aand the recombina. tion of the elements produced by such dissociation to produce a desired product.

In the apparatus illustrated lherein the hydrocarbon va iors, which leavethe upper end of the coil y the pi e 16, are led by a pipe 55 to the bottom o. an activating apparatus 5G which preferably is identical in construction with that provided for subjecting the oil to radioactivity and comprises a header 57 into which the hydrocarbon vapor is introduced and from which header the vapors ass through tubes 58 enclosing hars or tu es 59 containing radio-l active .material suoli fas uranium oxide in to a header 60 from which they may be conducted through a pipe 61vto the pipe 18 leading to the mixing chamber. The function4 of thisv activating apparatus is to place the hydrocarbon vapors in an activated condition male ing dissociation into simpler compounds more complete and capable of accomplishment with less expenditure of heat energy.

Desrably means are also provided by which the hydrocarbon vapors may be subjected alternatively to the action of the ultraviolet ray, or by means of which they may be subjected successively to emanations from a radioactive substance and to the ultraviolet ray. This is accomplished in the present invention by providing a branch pipe 62 leadpiel 16.

tube 66 which is super-- desired first to subject the l.

tions from a radioactive material and tliereafter to the action of the ultra-violet ray, a branch pipe 68 may be provided to connect the pipe 6l to the pipe 63,*tlie various pipes through which the hydrocarbon vapors are conducted being, of course, supplied with suitable valves as indicated to controlthe passage of the hydrocarbon in the desired inau'ner as will be readily understood by those skilled iu the art. Means are also preferably irovided to enable sumirhealeil .steam to lie introduced into the conduit Hi I'mthe highly heated hydrocarbon vapors so that a mixture of hydrocarbon vapor and 'steam may be subjected to the einanations ironia radioactive substance, or to the ulti'a-vioilet'ray, or both. This is conveniently accomplished by util izing the ivy-pass 19 connecting the pipe 17, through which the su perheater steam is discharged from the jacket, with the pipe 1G, through which the hydrocarbon va ors are discharged from the coil and provi( ing this by-pass with a suitable valve.70 throu h which. a regulated amount of steam may c supplied to the pipe 16, or which may be operated to prevent steam from entering the y reason of scribed, therefore, means are provided by which the hydrocarbon vapors alone, or the hydrocarbon -vapors mixed with superheated steam, may be selectively subjected to cmanations from a radoacti've'substance or to the action of the ultra-violet ray, or successively to both. Means are, therefore, provdcdfor securing a proper activation of the vapors or gases as may be most advantageous to the required dissociation of the molecules andthe chem ical reactions nectlie construction above dc-A lll) essary to produce the desired product from hydrocarbon oils of diil'erent characters and qualities.

A further object of the invention ,is to provide means for activating 'the supei'heated steam and facilitating the dissociation of it into its constituentelements, hydrogen and oxygen. This is accomplished in the pres ent invention by passing the snperheated steam through an apparatus having means to produce an action in the nature of a catalyst upon the superheated steam before it is mixing chamber.

introduced into the It has been found that where' steam 4is superheated to a high temperature the presence. of certain materialsz suchV as, nickel 'gauzeprei'erably in thc foi-in of a screen in a conduit;` through whiclitlie suerheateil steam is conducted, will facilitate t ie breakr 'ing up ol the steam into itsconstitnent velements particularly where the dissociatedelements are thereafter iiiiiiiediiitely associated with othery chemical elements or coniposi. tions, such as, unstable hydrocarbonvapors, with which the hydrogen and oxygen have a 4strong aliinit-y. For tliisreason tliematei-tial which promotes this actioii is referred to as' acting in the nature' ofa catalyst.-

. purposes of the present disclosure, usa com# bined catalytic and activating chainher, thei Asfillus'tratcd Vherein n branch pipe 7l leads from the. pipe 19 to the lower end ot a cl'ianibei'j 72 which will |be termed, for the lower portion of which cliamberis provided with a series of screens or grids 7 3 ot iilckel auze o'r other snitable'inaterial adapted lo iave an action upon the steam in the nature' of a catalyst which'will facilitate the dis- 'sociation of the steam. The upper portion of"thc combined catalytic 4and activating chamber 7 2 is provided with aseries of' tubes 74 each ofwhicli encloses a tube -or rod 75 containing a radioactive' substance, the sii.- pcrlijeated stcaiii oi' the products therefroii'i' passino upwardly'throiigh the tubes 74 into"` a hea e`r 76 and after-liaviiigbeeirtlius sub 'l jected to the ei'nanations froina radioactivesubstance are delivered from theheader E- through a pipe 77 to 'the conduit 18 which -leads to the mixing chamber. Another com- 'biiicdlcatalytic and activating chamber 78 desirably is also provided to .receive the slip-V erheated steam .which has been' passed f throu'gh the 'catalytic and activating chain-44 'ber land also to receive the hydrocarbon which hasbecn passed through the activate ing cliai'nber 56- and or the cliuinber-` G4 and subjected inthese chambers either to the.

emanations from .n alioactive substance or to the ultra-violet rxi-y` ortobotlL The chamber '-78' may be and preferably4 1s similar in all respects to the combined catalytic' and activating chamber 72.and the snperheated stcamand its' products, together with ,the hydrocarbon vapors, are sub]ected.

lto the aforesaid catalytic act-ionas well as to the 'ema'nation's from a radioactive sub-` stance in vtheir .intermingled condition rior ttheir introduction into the mixing c :im-

with Asuperhejited steuntV the purpose of which is to ina tain an ven heat upon the 'ed vapors and to prevent local heating jacket would be exposed to the direct heat'of the furnacel heated steam through a ranch pipe 8O lead- 79 lwhici is supplied with super-l pipe `18 leading tothe f by contact with the surface which otherwise ing from the pipe 17 through which superl heated steaniis" delivered trom the jacket.

' l`he steam from the jacket 79 of the mixing chamber desirably isdelivered through tion chamber throughout its entire lenfrth andv which may be controlled at wilhthus fil' . a. pipe 8l to a jacket' S2 completely surinsuring uniform and accurate' heat treatment of .the vapors or gases.v

. The-steainis conducted from lthe fixation chamber by a'. piie leading from the bot! tom thereof -aii which may be provided witha branch Sftextending through thewall vof the furnace and proi'fidedwith a. suitable shut-oil" `valveor may be' conducted throughabra'nch 8G leading tothe branch --be Vcontrolled in such-a manner that the required amount ofheat will be transmit-ted from the furnac'e through the steam jacket' to the fixation chamber `to maintain a constantv and uniform temperature upon the vapors or` gases whichI .are being treated in the fixation chamber.: Desirably the pipe 18, which conducts the hydrocarbon vapore or the mixture of hydrocarbon vapors and stea'in to the -xation chamberis providedwith a gauge 89 and with ,a b owao valve '90, and in order f urtlier to insure against accident the conduit '16, which delivers the hydrocarbon vapors frointhe coil; is pro-v vided with abi-anch pipe 91 having-a relief valve 92 to discharge the vapor in event .of excessive pressure. The fixed gases' which leave the fixationcliainber-throu h the pipe 30 desirably are f .conducted to tie first of a series of two or more expansion tanks 93 in which they are cooled tmore o'rless ,by expansion. "Any liquid 'which may-be condensed or produced bysuch expansion is1 collected'inthe -tank .and cana-bc withdrawn through lvalve-'controlled outlet conduits 94 and 95. These e provided with a suitpipe 19 which connnunicates with theblowi olt'ri the steam' delivery pipe '175 through' which bra uch pipe 1 9 the superheated steam 1nio nis

ils

llao

tanks -inay be arranged either in series 101 and within said furnace formed in a series ofor in parallel and any desired number of tanks may lbe employed. '.The gases are conducted from the last expansion tank by a conduit ,96 to the bottom of u, coil 97 which is, surrounded by a water jaeket98. In this coil the final liquid constituents ofthe gases are condensed and delivered to a catch tank 99 from which they may.' be removed through a valve-controlled conduit 100. -The cooled gases leave the top of the coil through a pipe ass through a meter 102 enroute to a gas holader or other suitable apparatus for storingor utilizing' the' gas.` Any dissolved. gas which may be carried down in to the eatch'tank' 99 by the liquid which l's-condensedin thecoil 97 may. be permittedto enter the main gas pipeV 101 through a branch pipe 103 leading from the upper portion of .the catch' tank 9 9 to the pipe 101.

" Having thus described the inventioinwhat 4is claimed as new, and desired t'o be secured by Letters Patent, is:

1. Anoil cracking and distillation apparatas comprising a. furnace, a jaeketed coil superposed substantially horizontal sections, means respectively for supplying oil vand water to the lower end of saidl coil and jacket, a header communicating with said oil-supplying means and having check .yalve control connection with said coil intermediate of itsV sections act-ing .to control the fluctuations of the liquid level of the oil in said coil.

2. An oil cracking and distillation apparatus comprising a furnace, al jacketed coil within said furnace formed in a series of Superposed substantially horizontal sections, means respectively .for supplying loil and water to the lower end of said coil 'and jacket, a header communicating withsaid water-supplying means and having check valve control connection with said coll jacket intermediate of the coil sections actinir to 'control 'the fluctuations of the liquid level of the oil in said coil. f 3. An oilcracking and distillation apparatus comprising a furnace, a jacketcd coil within said furnace formed in a series of superposed substantially horizontal sections, means respectively for supplying oil and water to the lower' end of said coil and jacket whereby the water will be converted into superheated steam and the oil heated, vaporized and its vapor superheated at substantially the same progressively increasinf .tem erature as that of the steam and cracker by t e heat of thefurnace, a jacketed mixing chamber within saidfurnace', a delivery conduitleading to said mixing lchamber' pro-' vided with branches connecting re'zpectively with said coil and jacket and means for supplyinfrsteam to the jacket of said mixing chamber whereby a high temperature will be maintained within the mixing chamber, but the walls retaunno said mixture proratus comprising a furnace, a. jacketed coil within said furnace formed in a series of superposed substantially horizontal sections i means respectively for supplying oil andwater to the lower end of said coil and jacket wherebyl the water will be converted into superheated steam andthe oil heated, vaporized and its vapor-superheated at suhstantially the same progressively increasing temperature as that ofthe steam and cracked by the heat of the furnace, a jaeketed mixing chamber within said furnace, a 'delivery conduit leading to said mixing chamber provided with branches connecting respectively with said coil and jacket and means for supplying superheated steam from the coil 'acket to t e mixing chamber jacket Wherey a hih temperature will be maintained within t e mixing chamber, but t-he Walls retaining said mixture -protected from the direct' heat of the furnace.

5. An' oil cracking and distillation apparatus com rising a furnace, a jacketed coil within sald furnace formed in a series of supcrposed substantially horizontal sections means respectively for supplying oil and water to the lower endof said coil and jacket whereby the water will be converted into superheated steam and the oil heated, vaporized and its vapor superheated at substantially the same progressively increasing temperature as that of the steam and cracked by the heat of the furnace, a jacketed mixing chamber within said furnace, means for supplying superheated steam to the jacket offsaid mixing chamber, a delivery conduit leading .to said mixing chamber provided with branches connecting respectively with said coil and jacket, a j acketed fixation chamber within said furnace communicating with said mixing chamber and means for supplymgsuperheated steam to the jacket of said fixation chamber.

(5.-An oil `crackin r and distillation apparatus comprising a tiurnace, a jacketed coil within said furnace formed in a series of superposed substantially horizontal sections, means respectively for supplying oil and water to the lower end of said coil and jacket whereby the water will be converted into super-heated steam and the oil progressively heated, vaporized and its vapor superheated at substantially the same progressively increasing temperature as that of the steam and cracked by the heat of the .furnace` a jacketed mixing chamber within said furnace, means for supplying superheated steam from the jacket of the coil lo the jacket of the mixing chamber.; a delivery conduit leading to said mixing chamber provided with branches connecting respectively with said Aum maracas.

coil and jacket, a jacketed fixation 'chamber within said furnace communicating with said -chainber and means for ;s upplying` superheated steanito thejacket of. said"xamixing tion chamber from' the jacket ofsadmixing chamber whereby-substantially uniform j'progressive heating of the-oil vapor and the steam envelope, which' surrounds it will be iii- Iratus comprising asured. .4 7. An oil cracking and distillation appa furnace,fa jacketed coil lwithin said furnace formed in a series oi superposcd substantially horizontal sections, l

means respectively oi' supplying oil and water tothe lower end ofvsaid coil.. and jacket whereby the water will be converted.

into superheated steam and the oil progressively heated, vaporized and its vapor superheated'at substantially 'the' same proufressively increasin r temperature as that o the steam and cracll chamber within said furnace, means for 'supplying-f` Vsupei'fheated steam from the jacket ot' tlieroil to the jacket of the inixin chamber, a delivery conduit leading to said-mixing chamber provided with branches connectin respectivelywith s'aidcoil and jacket, a 4jaclteted fixation chamber within said furnace communicate ing withsaid mixing 'chamber and means,

for supplying super-heated s teaiii` to the jacket of said fixation within said furnace formed in a series lof jackets (it-sait mixing chamber -and 'ci-aclezd jacketed mixing.' chamb'er within said iur chamber from the jacket of said mixing chamber and means for regulatino' the supply of steam to the and fixation chamber. v

8. An:oil cracking and distillation-apparatus comprising a furnace, a jacketed coil superposed substantially horizontal sections,

iueans respectively for supplying oil-4 and water to the lower end of said coil and jacket wlierebythe, water will be converted into superhcatedsteam and the oil progressively heated, vaporized and its vapor superheated'.' -at substantially the 'same 4progressively` inf4 that of ythe steamcreasing teinperature as y the heat of the,iurnace, ,a

nace,,meansdior supplying superheated steam "riim'thefacket .oithccoil to the acket oi ajdelivery con uit leadtheiriixin chamber,l

. ingto said mixingchamber provided with v within j said' 'fu'rnace said mix-"ling chamber,

branches connect-'ing respectively with said 'coil laii'd'jacke't, a j acketed fixation. chamber communicating `with means for supplying super-heated ,steam to' the jacket of .said fixirom the jacket of said mixing chamber, 'ineansior` regulating the sup- .ply of. steam 'to the' jackets of said mixing chamber and fixation I for regulating tie pressure of the super- 'heated steam in tbe'jackets of `said mixing' and fixation chambers whereby the ,temper- 'ratus comprising a furnace, within said urnacc formedl ,supcrposed substantially horizontal sections fthe heatof tl e furnace,

ed by the. heat. of the :Eurnace, a jacketed mixing chamber,

the jackets with said mixing chamber.

10,-- An oil crackin" and 'with said mixing duitlcading to said mixing chamber havingv said coils progressivelyv vmixing chamber and the jacket of #the ix.

chamber and means A atures maintained in the mixing and fixation chambers can be accurately controlled.

9. An oil cracking and distillation appaa jacketed coil in a series of means respectively lor `supplying oil an water tothe lower end of said coil and jacket whereby izedv and its vapor superheated at substaiitially the saine progressively increasing teinperature as that of the steam 4 and cracked by a Yjacketed mixing chamber within said furnace, means for supplying` superheated steaml from the jacket of. the-coil tothe jacket of the 'mixinr chamber,

a delivery: conduit 'leading to said mixing chamber provided with branches connecting res actively' with said coil andjacket, a.V

jac eted fixation chamber'within saiddurnace4 communicating 'with steam tothe. jacket of said fixation chamber from' the jacket of saidm'ixing chamber, means for regulating thejsu'p'ply of steam to latng valve, leading from Vthe jacket of said fixation chamber toone of Vthe branches of the delivery conduit which 'communicates distillation appa. ratas 'comprising a -iu a series of superposed substantially horizontal sectif'ins` means respectively fory supplying oil and watei-to the lower end ofsaid coil andjacket, a jiicketed mixing chamberconcen-4 tric-with said coil anda jacketed fixation 'chamber located beneath and comninnicating branches communicating respectively` with 4said coiland its jacketto introduce a mi ture of oil vapor and superheated steam into said mixing chamber and means for supplyf' ling snperheated steam from the jacket of to the 'jacket of the' ation chamber. 11. An oil cracking ratlis comprising a urnace, a jacketed coil `within said furnaceiormed in a seriesof .ture ofroil vapbr and superheated steam into the water will be4 converted. `into snperlieated steam and the oil heated, vaportov said. mixing means for supplying superheated l 'of said mixing chamber and fix- .atinncliamber 'and a conduit, having a reguilirnace' a. jacketed coil within said furnace :forme chainber,a delivery con' and distillation 'app'amixing chamber having said mixing chamber, means for 'supplyinfr superhcated steam from the jacket of sait coils progressively to the jacket of the mixing chamber and the jacket of the fixation chamber and means for delivering superheated steam from the jacket of the fixation chamber to the branch of the delivery conduit which leads to the mixing chamber.

12. An oil cracking and distillation apparatus comprising a furnace, a jacketed coil Vwithin said furnace 'formed in a series of superposedsubstantially horizontal sections,

means respectively for supplying oil and water to the lower end of said, coil and jacket, a jacketed mixing chamber 4and a jacketed fixation chamber communicating,r therewith and located in the furnace concentrically within said coil, an inlet conduit leading to said mixing chamber having branches connected respectively to said coil and its jacket to introduce a mixture of oil the lii'glly heated oil vapors from said con- A' oil within said duit to' said fixation chamber.

14. An oil cracking'and distillation apparatus comprising a furnace, a conduit for the, furnace, afixation chamber, means for. supplying oil to said conduit, means for preliminary heating the oil and subjecting the same to emanations from a radioactive, substance before entering said coi. A ,i

15. An oilcracking and distillation apparatus comprisin a furnace, 'a conduit for the cil within said urnace, a fixation chamber, means for supplying oil -to said conduit, means for preliminary heating the Voil and subjecting the same to emanations, from a radioactive substance" before entering saidv coil and means for subjecting the oilvapo delivered from said .conduit to. einanations from a radioactive substancebefore entering the fixation chamber.

16. An oil cracking and distillation apparatus comprising a' furnace, a conduit for the oil within said furnace, a fixation chainber, means for supplying oil to said conduit, means for conducting the highly heated orA vapor from said conduit to said fixation chamber and means for subjecting the oil vapor to emanations from a radioactive substance lbefore entering the fixation chamber.

17. An oil cracking `and distillation apparatus comprising a furnace, a conduit for the oil within said furnace, a fixation chamber, means for supplyme oil td said conduit,

means for conducting the highly heated oil vapor from said conduitto said fixation chamber and means for subjecting the oil vapor to the action of the ultra-violet ray a radioactive substance and to the action of the ultra-violet raybefore entering the fixation'chamber. i 19. An oil cracking and distillation 'plying oil and water respectively to said oil conduit and its jacket at the same end. whereby oil vapor and superheated steam of substantially the saine temperature will be progressively produced, a delivery conduit having branches communicatingI respectively with said conduit and its jacke-itl to receive the highly heated oil va or and superheated steam and means for su jecting the mixture of oil vapor and steam to a radioactive substance.

20. An oil crackingr and distillation apparatus comprising plying o'il and water respectively to said oil conduit and its jacket at the same end whereby oil vapor and superheated steam of. substantially the same temperature will be progressively produced, a delivery conduit having branches communicating"respectively with said conduit and itsl jacket to receive the highly heated oil vapor and superheated steam and meansfor subjecting said mixture of oil vapor and superheated steam to the action of the ultra-violet ray'.

21. An oil cracking and distillation apparatas comprising a furnace, a jacketed oil aPPa. ratus comprising a furnace, a jacketed o il conduit within said furnace, means for sup-- a furnace, a jacketed oil conduit Within said furnace,means for supemanations from conduit within said furnace, means for supplying oil and water respectively to said oil conduit and its jacket at the same end Whereby oil va or and superheated `steam Vof substantial y the same temperature-l will be progressively produced, adelivery conduit iaving branches communicating respectively with said conduit and its jacket to receive the highly heated oil vapor and superheatcd steam and means for subjecting said mixture' of oil vapor and superheated steam either to the einanations from a radioactive substance or to the action of ultra -violet ray or to both and a mixing chamber communicating with said delivery'r conduit.

29.. An oil cracking and distillatioi'i apparatus comprising means? for vaporizing Within said 1 furnace the oil and highly heating ythe vapor thereof, means for producing aiid-superlieating.

steam to substantially the same temperature as that of the oil vapor, mea-ns for subjecting a. portion of the superheated steam thus generated to. einanations from a radioactive substance andv means for'inixing the activated steam with the .oil vapor.

An oil cracking?1 and distillation apparatus comprising-means for vaporiznig the oil and highly .heating the 'vapor thereof, means for producing and siipeiheati'ng-.

steam to'siibstantially the Vsame temperature 'as that oftlie oilvapor, a niixiiigrl chamber,

means for introducing a mixture of highly heated oil vapor and a regulated amountl o f -the s'uperheatedL steam :.into said mixing chamber and means for sub]ecting another regulated amount of the steam to emanatio sl from a radioactive Asubstance and ad( ing the steain thus aetivatedto said mixture iii advance of the mixing: cl'ianiber.-

24. An oil'cracking and distillation apparatus comprising means for vaporizing the. oil and highlyheating the vapor thereof, means forfproduciiig and superlicatiiig` steam to substantially thesaine temperatureas that of the oil vapor, means for mixing.

` a portion; of the superheated steam with said oil vapor, means for4 subjecting said mixture toemanations from :a radioactive substance,

actvated'into saidmixturelp.

l26. An -oil cracking and' distillation 4ap-f y.par'atus comprising means for vaporizing.

. stance.

l the oil andliiglily of,.nieans for producing steam and supermeans for subjecting anotherportion of the 'steam to the einanations .frein-a radioactive substance and 'thereafter introducimfi;- the l paratus'coni steam,V thus activated 4into said mixture.

25. An oil cracking 'and distillationappai'atus comprising means. .for vaporizin'g4 the .oil and highly heating the vapor thereof-,`means forproducing and superli-eatingl .steam to substantially the same temperatora astl'iat of the oil vapor, means for mixing a I portion ofthe superheated steiimwith said. oil vapor, means-for subjectin said mixture to the .action of the ultra-vio et ray, means for subjecting another portion ofthe steam to eniani'itior'is from a radioactive'substance and .thereafter introducing. the stearnthus V the oil and highly heat-ing the vapor there-" 4of, means 'for producing steanifand superheating the saine to substantially the same temperature as that of the oil vapor, -ineans for mixing a portion thereof. with said oil vapor, means for subjecting the oil before4 vapor-ization to emanations from a radioactivesubstance and means forsubjecting lthe"inixture of oil vapors and Qsupegrlieate from a radioactive sub ing the highly steam to emanations 27,' An .oil paratus .comprising means for. vaporizing heating the vapor there eniaiiations .from

cracking and distillation ap heating the vsaine to substantially the same temperature ofthe oil vapor and means for mixing a portion thereof with said oil va or..`

aiiz'l means for subjecting. the .water be ore vaporization into steam to en'ianations from a radioactive siibstaiice.`

28. An oil cracking' and distillation ap-` i 'parati'is roiiiprising means for -vapoi'izing the oil and highly heating the vapor'thereof, means for pi'oduciiigstea-ni and superiii A Y heating tl'ie same to substantially the same tciiipc'rature asthat o f the oi-ll vapor, means -for mixing a portion thereof with said oil vapor, means for respectively subjecting the' -u'ater-aiid oil before vaporization to emanations from a radioactive substance and .ineansvfor subjecting the mixture of oil' vapor and superheated steam to emanatio'ris from a radioactive substance. y

Zik-Anil cracking and-distillation apparatus comprising-means for -'vaporizing' heating lthe saine to" substantially the same tei'nperatiire as Vthat of the oil vapor, means the oil and highlylieatingthe .vapor there-v of; 4means for producing' steam and siipei4 for mixing a -)ortioii' thereof with said oil' vapor, means or iespectivelysiibwcting the' -water and oil before vaporization to emanations from a radioactive "substance and. en

the 'mixture of oil vapor and superheatedV steam.selectively to An oil cracking' inid .distillation .a rising means for vaporiziiig t e oil and hig' y .heating.tlievapoithereoh .a radioactive substance orV to the action of the'ultr'a-violet ray'or both.

ico

means for reducing and superli'eating steam to substantially the same temperature as that' of the oil vapor, means for'subjecting a por `tion ofthe superheated 'stream tothe iniiii'ence of 'a su stance capable'of catalyticlike action upon said superheated steam to i facilitate Vdissociationthereoineans. for subjeeting' th'esteam and the elements dissociated-therefrom and intermingled therewith.

to the] activating iniluence Vof emanations ',f' from a radioactive siibstanceand means for mixin theactivated superheated. steam and said issociated elements' with heated hydrocarbon vapors.

" 31. An oil cracking and distillation appaltion of the superheated's'team to theinthience of a substance capable of catalytic-like ac-l I Vtion uion said superheated steam to facilitate dissociatioii't iereof, means for subjectheated hydrocarbon vapors to the -eiiianations of a radioactive substance and means for' mixing the activated hydrocarbon vapors with the sii'perheatedsteam.tl and itsdissociated elements. f

.oil and highly heating the ofa substance capable of catalytic-like action.

upon said superheated .steam to facilitate dissociation thereof, means for subjecting the highly heatedhydrocarbon ,vapors to the annulations 'of a. radioactive substance and also to the activating influence of the ultra'- violet ray and means for mixing the actirated hydrocarbon vapors with the superheated steam and its dissociated elements.

33. An oilcracling and distillation apparatus comprising means for vaporizing the vapor thereof; means for producing and super]ieatingsteam to substantially the same temperature-as 'that 'to the ultraviolct ray or of the oil vapor, means for suibjecting a portion of the superheated steam to the influence therefrom and interminglecl therewith to the i activating influence' ot' einanations from a vadioactive substance, means for mixing an other portion of the su )erheatecl steuni with Said. highly lheated hydl for subjecting said mixture selectively to emanations from'a radioactive substance or to 'both and means for mixing the activated mixture with the activated snperheated steam and its dissociated elements. Y

In testimony whereof, nume to this specification.

STEPHEN L; TINGLEY.

I have sifrned m 

